Technical field of the invention
[0001] The present invention relates to the field highly hydrophobic and superhydrophobic
coatings.
Background of the invention
[0002] Hydrophobic, highly hydrophobic and superhydrophobic coatings can be used for many
kinds of surfaces. In the art many approaches have been used to manufacture highly
hydrophobic coatings.
[0003] US 2006/0141223 A1 relates to textile sheet-like constructions having enhanced watertight properties
and to a process for producing them. This fiber modification process requires solvent.
[0004] WO 2001/062863 A1 relates to an aqueous laquer dispersion suitable for hydrophobic coatings. The material
is mainly carboxylated polystyrene pigments, wherein part of the carboxylic groups
are esterified with fluorinated aliphatic alcohols.
[0005] US 2006/0257643 A1 describes a method of producing hydrophobic composites and aggregates. The process
requires several process steps and is not suited to preparing continuous coatings.
[0006] The published French patent application
FR 2 852 966 discloses an aqueous composition for treating surfaces and making them superhydrophobic,
comprising a thermoplastic polymer in an aqueous emulsion and mineral particles having
a size from 5 to 500 µm. The mineral can be for instance calcium carbonate, quartz,
mica, talc, titanium dioxide, barium sulphate, calcium sulphate etc. The polymer can
be for instance polystyrene, polymethacrylate, polyvinyl butyral, and polyurethane.
[0007] US 6,712,932 discloses a paper or a paper-like material with a structure, comprising particles
of, for instance, metal oxides and carbonates, which are fixed to the paper by means
of a wet-laying method using a binder together with a water-repelling agent.
[0008] US 6,660,363 discloses a self-cleaning surface comprising elevations made of hydrophobic polymers
or permanently hydrophobized materials.
[0009] US2005/0136217 A1 discloses a self-cleaning object with a layer of hydrophobic material having protrusions
and recesses, which layer is applied with a solution, dispersion or emulsion containing
hydrophobic material and a liquid where the liquid is evaporated. The mixture may
also comprise other solid particles.
[0010] US 2006/0257643 discloses hydrophobic composites, particularly hydrophobic particulates and free-flowing
aggregates and methods utilizing the same.
[0011] Highly hydrophobic wet-laid coatings may be divided into two main types of coating
treatments, either solvent-borne or water-borne. Solvent-borne treatments are subject
to controls or regulatory limitations in some countries. On the other hand, water-borne
coating treatments are usually more difficult to implement in order to obtain hydrophobic
coatings and thus more limited than solvent-borne coating treatments, due to the dual
requirement for a stable coating dispersion in the aqueous phase and for hydrophobicity
in the dry state of the final coating layer. In particular, the application of the
superhydrophobic coating often involves multiple steps by creating surface structure
and low surface energy coating in different steps. Moreover, standard oil-in-water
emulsion-based strategies for encapsulating and delivering hydrophobic species tend
to leave an emulsifier (e.g. surfactant) on the coated surface upon drying, which
in turn tends to enhance wetting.
[0012] Other disadvantages of prior art methods is that they may involve toxic components,
that coatings may be made of expensive materials and cannot easily be applied to for
instance paper using existing processes and equipment. Other problems in the prior
art related to highly hydrophobic coatings include the use of silane treated and/or
fluorinated components, which are expensive and may have negative impact on environment
in both producing the components and during the life cycle of the coatings containing
these components. Another problem in the prior art is that hydrophobic coatings require
multiple steps for the application, which often leads to use of more material and
a more complicated process for the application. Thus there is a need for an alternative
coating composition, which would be effective in rendering surfaces hydrophobic without
having the above-mentioned drawbacks.
Summary of the invention
[0013] The present invention relates to an aqueous dispersion to be used in the manufacture
of a hydrophobic coating, said aqueous dispersion comprises inorganic particles, at
least one fatty acid or a salt thereof, a polymeric binder, and water.
[0014] The present invention moreover relates to a method for preparing an aqueous dispersion
comprising the step of mixing an aqueous dispersion of a polymeric binder with a mixture
of inorganic particles and at least one fatty acid or a salt thereof.
[0015] The present invention further relates to a method for coating a substrate comprising
contacting said substrate with an aqueous dispersion according to the invention.
[0016] The present invention further relates to objects and substrates coated according
to the present method.
[0017] Further embodiments of the present invention are defined in the appended dependent
claims, which are specifically incorporated by reference herein.
[0018] It is one object of the present invention to obviate at least some of the disadvantages
in the prior art and provide an improved method for coating an object with a hydrophobic
coating, and provide an aqueous dispersion and objects coated with the improved method.
Thus advantages of the present invention include that the coating can be applied in
one step, it is non-toxic, safe for food packaging, and relatively environmentally
friendly and inexpensive. A further advantage is that existing industrial coating
processes can be used for applying the coating. Another advantage is that it is possible
to obtain highly hydrophobic or superhydrophobic coatings without silanes or fluorinated
components.
Definitions
[0019] Before the invention is disclosed and described in detail, it is to be understood
that this invention is not limited to particular configurations, process steps and
materials disclosed herein as such configurations, process steps and materials may
vary somewhat. It is also to be understood that the terminology employed herein is
used for the purpose of describing particular embodiments only and is not intended
to be limiting since the scope of the present invention is limited only by the appended
claims and equivalents thereof.
[0020] It must be noted that, as used in this specification and the appended claims, the
singular forms "a", "an" and "the" include plural referents unless the context clearly
dictates otherwise.
[0021] The term "about" as used in connection with a value throughout the description and
the claims means that the true value can be up to 10% higher or down to 10% lower
than the indicated value.
[0022] If nothing else is defined, any terms and scientific terminology used herein are
intended to have the meanings commonly understood by those of skill in the art to
which this invention pertains.
[0023] The following terms are used throughout the description and the claims.
[0024] "Acicular" is used herein to denote a needle-like shape.
[0025] "Antioxidant" as used herein denotes a substance capable of preventing, slowing down,
or suppressing oxidation.
[0026] "Apparent density" as used herein denotes dry mass per unit volume of a material
including voids inherent in the material.
[0027] "Aqueous dispersion" as used herein encompasses a mixture comprising water.
[0028] "Base" as used herein denotes a functional group with the ability to take up a proton.
[0029] "Biocide" as used herein denotes a substance capable of preventing, slowing down,
or suppressing growth of living organisms.
[0030] "Coalescence agent" as used herein denotes an agent that causes or promotes coalescence.
[0031] "Crosslinks" as used herein denotes any bonds linking one polymer chain to another.
[0032] "D
50" as used herein denotes the 50
th percentile of the mass-weighted size distribution of particles. Accordingly 50 %
of the inorganic particles have a size greater than D
50 and 50 % of the inorganic particles have a size of less than D
50. The particle size is determined for the primary particles if the particles are not
aggregated in larger agglomerates, but if the particles are aggregated in larger agglomerates
the size of the agglomerates is measured.
[0033] "Defoaming agents" as used herein denotes a substance capable of preventing, slowing
down, or suppressing foaming.
[0034] "Inorganic particle" as used herein denotes a particle comprising inorganic material,
although small amounts of organic material may be present.
[0035] "Fungicide" as used herein denotes a substance capable of preventing, slowing down,
or suppressing growth of fungi.
[0036] "Highly hydrophobic" is used herein to denote a surface with an equilibrium contact
angle between 120 degrees and 150 degrees for a drop of water on the surface.
[0037] "Hydrophobic" as used herein denotes the property to repel water. A hydrophobic surface
is a surface with a contact angle of more than 90 degrees but less than 120 degrees.
[0038] "Inorganic particle" as used herein encompasses an inorganic particle of any shape.
[0039] "Optical brighteners" as used herein denotes dyes that absorb light in the ultraviolet
and violet region of the electromagnetic spectrum and re-emit light in the blue region.
[0040] "Polymeric binder" as used herein denotes a binder that is a polymer.
[0041] "Rheology modifiers" as used herein denotes a substance with the capability to modify
rheological properties of a fluid.
[0042] "Scalenohedral" as used herein denotes a pyramidal form under the rhombohedral system,
enclosed by twelve faces, each a scalene triangle.
[0043] "Substance" as used herein denotes a pure or a non-pure chemical compound or a mixture
of chemical compounds, thus a for instance mineral is encompassed within the term.
[0044] "Superhydrophobic" as used herein denotes a surface with an equilibrium contact angle
higher than 150 degrees for a drop of water on the surface.
Detailed description of the invention
[0045] According to the present invention there is provided an aqueous dispersion to be
used in the manufacture of a hydrophobic coating, said aqueous dispersion comprises:
inorganic particles, at least one fatty acid or a salt thereof, a polymeric binder,
and water.
[0046] The amounts of the components in the aqueous dispersion are
• from about 20 to about 55 wt%, preferably from about 30 to about 45 wt%, most preferably
from about 30 to about 40 wt% of inorganic particles,
• from about 0.1 to about 2 wt%, preferably from about 0.5 to about 1 wt%, most preferably
from about 0.7 to about 0.8 wt% of at least one fatty acid or a salt thereof, and
• from about 5 to about 20 wt%, preferably from about 8 to about 15 wt%, most preferably
from about 10.5 to about 12 wt% of a polymeric binder,
• the rest being water and optional additives.
[0047] The inorganic particles according to the present invention have an apparent density
from about 0.30 g/ml to about 4 g/ml, a BET specific surface area from about 1 to
20 m
2/g, and a D
50 less than about 20 µm.
[0048] In one embodiment of the present invention the inorganic particles the following
properties:
• Apparent density from about 0.30 g/ml to about 2.7 g/ml, preferably from about 0.30
g/ml to about 0.80 g/ml and most preferably about 0.30 g/ml to about 0.65 g/ml.
• BET specific surface area from about 1 to 20 m2/g, preferably more than about 3 m2/g and more preferably more than 5 m2/g.
• D50 less than about 20 µm, preferably from about 1 to about 10 µm, most preferably from
about 2 to 5µm.
[0049] In an alternative embodiment, of the present invention the inorganic particles the
following properties:
• Apparent density from about 1 g/ml to about 4 g/ml, preferably from about 2 to about
3.5 g/ml and most preferably about 2.5 g/ml to about 2.9 g/ml.
• BET specific surface area from about 1 to 20 m2/g, preferably more than about 6 m2/g and more preferably more than 9 m2/g.
• D50 less than about 10 µm, preferably from about 0.1 to about 5 µm, most preferably from
about 0.2 to 2µm.
[0050] The inorganic particles used in the present invention may comprise a mixture of different
inorganic particles with different properties.
[0051] The inorganic particles used in the invention are preferably basic. Either the inorganic
particles can be intrinsically basic or alternatively they may be treated to obtain
basic functional groups on the surface. If the method uses non-basic inorganic particles
it is preferred to treat the inorganic particles so that they exhibit basic groups
on the surface. Examples of such treatment include contacting said inorganic particles
with an aqueous solution of at least one hydrolysable polyvalent metal salt, followed
by neutralisation. The treatment is preferably carried out before the fatty acid or
salt thereof is coated on the inorganic particles.
[0052] The inorganic particles used in the present invention in one embodiment comprise
at least one substance selected from the group consisting of calcium carbonate and
kaolin.
[0053] The inorganic particles used in the present invention in one embodiment comprise
at least one substance selected from the group consisting of anatase, calcinated clay,
kaolin, and talc, the surface of which has been made basic.
[0054] The inorganic particles used in the present invention in one embodiment comprise
at least one substance selected from the group consisting of aluminium hydroxide,
aragonite, barium sulphate, calcite, calcium sulphate, dolomite, magnesium hydroxide,
magnesium carbonate, magnesite, titanium dioxide (rutile), and vaterite.
[0055] The inorganic particles used in the present invention in one embodiment comprise
at least one substance selected from the group consisting of zincite, corundum, hematite,
magnetite, ilmenite, and cassiterite.
[0056] The inorganic particles used in the present invention in one embodiment comprise
at least one substance selected from the group consisting of dispore, boehmite, goethite,
lepidocrocite, rhodocrosite, siderite, baryte, strontianite, apatite, feldspar and
fluorite.
[0057] The inorganic particles used in the present invention in one embodiment comprise
SiO
2.
[0058] Other examples of inorganic particles include at least one substance selected from
the group consisting of anatase, calcinated clay, kaolin, and talc, wherein the surface
of said inorganic particles has been made basic. If the particles are not intrinsically
basic they need to be treated by any suitable method to make them basic.
[0059] The inorganic particles are preferably calcium carbonate particles, more preferably
precipitated calcium carbonate and most preferably aragonite.
[0060] The inorganic particles are surface treated with a fatty acid or a salt thereof.
Advantages of using one or more fatty acids are that fatty acids are inexpensive compared
to silanes and fluorinated polymers and are readily available and used in many industries.
Fatty acids interact in a suitable way with inorganic particles such as calcium carbonate
and many fatty acids are approved for contact with food. The inorganic particles are
coated by contacting them with an aqueous solution or dispersion comprising a fatty
acid or a salt thereof. The aqueous solution or dispersion can be the same as the
aqueous dispersion that comprises the binder. Alternatively the coating can be performed
in a separate aqueous solution or dispersion. Preferably the coating of the inorganic
particles is performed in a separate aqueous solution or dispersion. The inorganic
particles can optionally be coated with several different fatty acids of salts thereof,
optionally in several steps. The fatty acid or salt thereof forms a layer on the entire
inorganic particle surface; alternatively the fatty acid or salt thereof forms a layer
on a part of the surface. Optionally the coating comprises surfactants. The amount
of fatty acid or salt thereof should be high enough so that the inorganic particles
become dispersible in water. A suitable amount of fatty acid generally corresponds
to a double layer of molecules on the surface of the inorganic particles. Thus the
inorganic particles become dispersible in water or alternatively the ability to be
dispersed in water is improved.
[0061] In one particularly preferred embodiment inorganic particles comprising calcium carbonate,
are treated with stearic acid.
[0062] Inorganic particles with relatively poor packing are preferred, which yields a suitable
roughness of the coating. Inorganic particles with narrow particle size distribution
are also preferred, possibly combined with a tendency to aggregate to larger secondaries.
Preferably the inorganic particles are acicular or scalenohedral. The shape of the
particles is however not limited to these two shapes. Also other thorny, spiky and
needle like shapes are preferred for use according to the present invention. Other
possible shapes include chestnut husk shapes.
[0063] Particles with a preferred shape have small size, low density and high specific surface.
[0064] Preferably inorganic particles without any appreciable residues of dispersants are
used. Examples of such undesired dispersants include sodium polyacrylate polymers
and copolymers.
[0065] Acicular aragonite is one preferred choice for the inorganic particles, especially
acicular aragonite with a D
50 from about 0.1 to about 20 µm, preferably from about 0.2 to about 10 µm. In alternative
embodiments, a combination of PCC (precipitated calcium carbonate) or GCC (ground
calcium carbonate) products having different particle size distributions is used.
[0066] A saturated or unsaturated fatty acid or salt thereof is used. A fatty acid or salt
thereof with linear or branched hydrocarbon chain is used. Preferably the fatty acid
or salt thereof has 8 to 22, more preferably 10 to 18 carbon atoms. Particularly preferred
fatty acids are selected from the group consisting of oleic acid, stearic acid and
palmitic acid. Also preferred are salts of the latter fatty acids. The counter ions
of a fatty acid salt can be any suitable ion. Examples include a sodium ions and ammonium
ions, which are common and inexpensive salts.
[0067] Examples of preferred binders include carboxylated latex, styrene-butadiene latex
and styrene acrylate. Such carboxylated latex is a latex or emulsion polymer stabilised
predominantly by carboxylation. Preferably the glass transition temperature of the
binder is in the range from about -40 to about 50°C, and more preferably from about
0 to about 50°C. Examples of a polymeric binder include commercially available binders
supplied by Dow Chemical Company under the trade name DL 940 or experimental latex
Dow/HPQ73 or by Rhodia under the trade name Ultradia 7100, 7300 or 7400.
[0068] A synthetic latex, as is well known, is an aqueous dispersion of polymer particles
prepared by emulsion polymerization of one or more monomers.
[0069] The monomer composition employed in the preparation of the latex comprises from about
10 to 95 pphm of a first monomer (A), from about 40 to 90 pphm of a second monomer
(B), and from 0 to about 5 pphm of a functional monomer (C). As used herein, the term
"pphm" means parts per hundred monomer, a term well known to those skilled in the
art. Accordingly, the total parts monomer employed is 100 parts monomer, on a weight
basis.
[0070] The first monomer (A) is a low Tg monomer comprising an alkyl acrylate or butadiene.
The low Tg monomer is used in amounts of from about 10 pphm to about 95 pphm, preferably
15 pphm to 40 pphm. Examples of low Tg monomers include monomers having a Tg of less
than 10°C that are C
1 -C
10 alkyl esters of acrylic acid, C
2 -C
10 alkyl esters of alpha, beta-ethylenically unsaturated C
4 -C
6 monocarboxylic acids, C
4 -C
10 dialkyl esters of alpha, beta-ethylenically unsaturated C
4 -C
8 dicarboxylic acids, and vinyl esters of carboxylic acids, including, without limitation,
vinyl isobutyrate, vinyl-2-ethyl-hexanoate, vinyl propionate, vinyl isooctanoate and
vinyl versatate and butadiene. The low Tg monomer can be selected from the group consisting
of C
1-C
10 alkyl esters of (meth)acrylic acid, i.e. alkyl (meth)acrylates, and C
4 -C
8 dialkyl esters of maleic, itaconic and fumaric acids. Preferably, at least one C
2 -C
8 alkyl ester of acrylic acid is utilized. Particularly preferred low Tg monomers include
ethyl acrylate, butyl acrylate, 2-ethyl hexyl acrylate, decyl acrylate, dibutyl maleate,
dioctyl maleate, and butadiene with butadiene being most preferred. Mixtures of first
monomers can be employed.
[0071] The second monomer (B) is a high Tg monomer having a Tg greater than 10°C such as,
for example, vinyl esters of carboxylic acids, the acid having from two to about 13
carbon atoms and styrene. Representative high Tg comonomers include methyl methacrylate,
dimethyl maleate, t-butyl methacrylate, t-butyl isobornyl acrylate, phenyl methacrylate,
acrylonitrile and vinyl esters of carboxylic acids having Tg of greater than 10°C
and styrene.
Examples of such vinyl esters include vinyl pivalate, vinyl neodecanoate, vinyl neononanoate,
and mixtures of branched vinyl esters such as the commercially available VeoVa 11
and EXXAR Neo-12. The second monomer advantageously is employed in an amount of from
about 40 pphm to about 90 pphm, preferably 60 pphm to 85 pphm. Mixtures of high Tg
comonomers can be employed.
[0072] It may also be desired to incorporate in the binder polymer minor amounts of one
or more functional comonomers (C). Suitable copolymerizable comonomers (C) include,
for example: acrylic acid; methacrylic acid; itaconic acid; fumaric acid ; the half
esters of maleic acid, such as monoethyl, monobutyl or monooctyl maleate; acrylamide;
tertiary octylacrylamide; N-methylol (meth)acrylamide; N-vinylpyrrolidinone; diallyl
adipate; triallyl cyanurate; butanediol diacrylate; allyl methacrylate; etc.; as well
as C
2 -C
3 hydroxyalkyl esters such as hydroxyethyl acrylate, hydroxy propyl acrylate and corresponding
methacrylates. The comonomer (C) generally is used at levels of less than 5 pphm,
preferably less than 2.5 pphm, depending upon the nature of the specific comonomer.
Mixtures of comonomer (C) can be employed.
[0073] In addition, certain copolymerizable monomers that assist in the stability of the
binder, e.g., vinyl sulfonic acid, sodium vinyl sulfonate, sodium styrene sulfonate,
sodium allyl ether sulfate, sodium 2-acrylamide-2-methyl-propane sulfonate (AMPS),
2-sulfoethyl methacrylate, and 2-sulfopropyl methacrylate, can be employed as emulsion
stabilizers. These optional monomers, if employed, are added in very low amounts of
from 0.1 pphm to about 2 pphm.
[0074] Methods for preparing synthetic latexes are well known in the art and any of these
procedures can be used.
[0075] Suitable free radical polymerization initiators are the initiators known to promote
emulsion polymerization and include water-soluble oxidizing agents, such as, organic
peroxides (e.g., t-butyl hydroperoxide, cumene hydroperoxide, etc.), inorganic oxidizing
agents (e.g., hydrogen peroxide, potassium persulfate, sodium persulfate, ammonium
persulfate, etc.) and those initiators that are activated in the water phase by a
water-soluble reducing agent. Such initiators are employed in an amount sufficient
to cause polymerization. As a general rule, a sufficient amount is from about 0.1
to about 5 pphm. Alternatively, redox initiators may be employed, especially when
polymerization is carried out at lower temperatures. For example, reducing agents
may be used in addition to the persulfate and peroxide initiators mentioned above.
Typical reducing agents include, but are not limited to: alkali metal salts of hydrosulfites,
sulfoxylates, thiosulfates, sulfites, bisulfites, reducing sugars such as glucose,
sorbose, ascorbic acid, erythorbic acid, and the like. In general, the reducing agents
are used at levels from about 0.01 pphm to about 5 pphm.
[0076] The emulsifying agents are those generally used in emulsion polymerization. The emulsifiers
can be anionic, cationic, surface-active compounds or mixtures thereof.
[0077] Suitable nonionic emulsifiers include polyoxyethylene condensates. Exemplary polyoxyethylene
condensates that can be used include polyoxyethylene aliphatic ethers, such as polyoxyethylene
lauryl ether and polyoxyethylene oleyl ether; polyoxyethylene alkaryl ethers, such
as polyoxyethylene nonylphenol ether and polyoxyethylene octylphenol ether; polyoxyethylene
esters of higher fatty acids, such as polyoxyethylene laurate and polyoxyethylene
oleate, as well as condensates of ethylene oxide with resin acids and tall oil acids;
polyoxyethylene amide and amine condensates such as N-polyoxyethylene lauramide, and
N-lauryl-N-polyoxyethylene amine and the like; and polyoxyethylene thio-ethers such
as polyoxyethylene n-dodecyl thio-ether.
[0078] Nonionic emulsifying agents that can be used also include a series of surface active
agents available from BASF under the PLURONIC and TETRONIC trade names. In addition,
a series of ethylene oxide adducts of acetylenic glycols, sold commercially by Air
Products under the SURFYNOL trade name, are suitable as nonionic emulsifiers.
[0079] Representative anionic emulsifiers include the alkyl aryl sulfonates, alkali metal
alkyl sulfates, the sulfonated alkyl esters, and fatty acid soaps. Specific examples
include sodium dodecylbenzene sulfonate, sodium butylnaphthalene sulfonate, sodium
lauryl sulfate, disodium dodecyl diphenyl ether disulfonate, N-octadecyl sulfosuccinate
and dioctyl sodiumsulfosuccinate. The emulsifiers are employed in amounts effective
to achieve adequate emulsification of the polymer in the aqueous phase and to provide
desired particle size and particle size distribution.
[0080] Other ingredients known in the art to be useful for various specific purposes in
emulsion polymerization, such as, acids, salts, chain transfer agents, chelating agents,
buffering agents, neutralizing agents, defoamers and plasticizers also may be employed
in the preparation of the polymer. For example, if the polymerizable constituents
include a monoethylenically unsaturated carboxylic acid monomer, polymerization under
acidic conditions (pH 2 to 7, preferably 2 to 5) is preferred. In such instances the
aqueous medium can include those known weak acids and their salts that are commonly
used to provide a buffered system at the desired pH range.
[0081] Various protective colloids may also be used in place of or in addition to the emulsifiers
described above. Suitable colloids include casein, hydroxyethyl starch, carboxyxethyl
cellulose, carboxymethyl cellulose, hydroxyethylcellulose, gum arabic, alginate, poly(vinyl
alcohol), polyacrylates, polymethacrylates, styrene-maleic anhydride copolymers, polyvinylpyrrolidones,
polyacrylamides, polyethers, and the like, as known in the art of emulsion polymerization
technology. In general, when used, these colloids are used at levels of 0.05 to 10%
by weight based on the total weight of the reactor contents.
[0082] The manner of combining the polymerization ingredients can be by various known monomer
feed methods, such as, continuous monomer addition, incremental monomer addition,
or addition in a single charge of the entire amounts of monomers. The entire amount
of the aqueous medium with polymerization additives can be present in the polymerization
vessel before introduction of the monomers, or alternatively, the aqueous medium,
or a portion of it, can be added continuously or incrementally during the course of
the polymerization.
[0083] Final particle size of the latex can vary from 30nm to 1500nm.
[0084] The amount of binder must be high enough so that the coating exhibits the desired
adhesion, mechanical strength and hydrophobicity, but on the other hand the amount
of binder must not be too high so that the hydrophobicity of the coating is reduced
by the binder submerging the inorganic particles. A person skilled in the art can
in the light of this description adjust the amount of binder within the range of the
appended claims.
[0085] The degree of carboxylation for carboxylated latex should be adapted relative to
the amount of fatty acid in the coating composition. It is undesired that the total
number of carboxyl groups of the binder is higher than the total number of carboxyl
groups of the fatty acid. Therefore, in general, low-carboxylated latex should perform
best for low amounts of fatty acid.
[0086] The process for making the above-defined coating composition can be carried out in
several ways according to the present invention. The process comprises the step of
mixing an aqueous solution of a polymeric binder and a mixture of fatty acid and inorganic
particles. The process also comprises the step of coating the inorganic particles
with a fatty acid. Said coating occurs in the mixture of fatty acid and inorganic
particles.
[0087] Thus there is provided a method for preparing an aqueous dispersion comprising the
step of mixing an aqueous dispersion of a polymeric binder with a mixture of inorganic
particles and at least one fatty acid or a salt thereof.
[0088] In one embodiment the mixture of inorganic particles and at least one fatty acid
or a salt thereof is prepared by
- a) mixing said at least one fatty acid or a salt thereof with water,
- b) mixing said inorganic particles with water, and then
- c) mixing the mixtures from step a) and step b).
[0089] In an alternative embodiment said mixture of inorganic particles and at least one
fatty acid or a salt thereof is prepared by
a)mixing at least one fatty acid or a salt thereof with water, and then
b)mixing the mixture from step a) with said inorganic particles.
[0090] In a preferred embodiment the polymeric binder is mixed with said inorganic particles
at least 15 minutes after the mixing of said at least one fatty acid or a salt thereof
with said inorganic particles.
[0091] Optionally the aqueous dispersion according to the present invention comprises surfactants.
If a surfactant is used in the aqueous dispersion it can be added before, at the same
time as, or after the fatty acid or salt thereof. An optional surfactant can also
be added before, at the same time as, or after the polymeric binder. The surfactant
is preferably chosen so that it does not adversely affect the coating. Cationic surfactants
are less preferred. Examples of surfactants include phosphoric acid alkyl ester and
diphosphonate surfactants, silicone based surfactants, fluorosurfactants, or salts
thereof.
[0092] Optionally the aqueous dispersion comprises other additives. Examples of such additives
include antioxidants, biocides, coalescence agents, coloured inorganic particles,
crosslinkers, defoaming agents, dyes, coalescence agents, fungicides, lubricants,
optical brighteners, rheology modifiers, or any combination thereof. Preferably such
additives should be compatible with the other components of the aqueous dispersion.
[0093] The present invention provides a method for coating a substrate with a highly hydrophobic
or superhydrophobic coating comprising: a) preparing an aqueous dispersion, b) contacting
said substrate with said aqueous dispersion. Thereby the surface of a substrate is
rendered hydrophobic, highly hydrophobic or superhydrophobic.
[0094] The aqueous dispersion as described above is contacted with the substrate to be coated.
After contacting the substrate with the aqueous dispersion the substrate is dried.
The thickness of the dried coating on the substrate is from about 3 to about 40µm,
preferably from about 8 to about 25µm. The amount of polymeric binder depends on several
variables including the surface area of the inorganic particles. The larger the surface
area, the more polymeric binder is required for strength properties.
[0095] After the substrate has been contacted with the aqueous dispersion according to the
present invention it can optionally be heated. Heating is particularly useful if a
short drying time and high process speed is needed. The properties of the polymeric
binder can be improved by curing by heat. If paper or paper-like material is the substrate,
heating can be useful to decrease the water content of the coated paper. As an alternative
to heating the object can be dried without additional heating. A combination of drying
and heating can also be used.
[0096] The coating according to the present invention may be applied to a large variety
of substrates.
[0097] According to the present invention there is provided objects coated with the method
according to the present invention.
[0098] Coating for medical devices is possible.
[0099] Preferably the coating according to the present invention is highly hydrophobic,
i.e. it displays an equilibrium contact angle between 120 degrees and 150 degrees.
More preferably the contact angle is higher than 135 degrees.
[0100] Using the present invention it is even possible to manufacture superhydrophobic coatings,
which display an equilibrium contact angle greater than 150 degrees.
[0101] Advantages of the present invention are that the coating can be applied in one step,
it is non-toxic, approved for food contact, inexpensive and it can be produced in
an environmentally friendly manner. A further advantage is that existing industrial
coating processes can be used for applying the coating. Another advantage is that
a hydrophobic surface is created without any need for stamping or etching.
[0102] It is to be understood that this invention is not limited to the particular embodiments
shown here. The following examples are provided for illustrative purposes and are
not intended to limit the scope of the invention since the scope of the present invention
is limited only by the appended claims and equivalents thereof.
Examples
[0103] The following methods apply to all examples mentioned below.
Dry stain size measurement
[0104] In the stain test 5 drops of an exact amount (9µl, i.e. drop diameter 2.58 mm) of
a blue dye aqueous solution are auto-pipetted (from a fixed height of 1.9 mm from
drop bottom to coat surface) on the coated surface. The blue dye is added to aid visual
inspection of stain size after complete evaporation of the water. The surface tension
of the colored water is the same as the non-colored deionized water. The samples are
stored at 23°C and 50% relative humidity, and the final size of the dry stain after
complete evaporation is measured with a sliding gauge, both in machine direction MD
and cross direction CD. The values given below correspond to the mean of the set of
5 drops measured in these two directions. They are expressed in a dimensionless form
by dividing the stain diameter by the drop diameter prior to contact (i.e. 2.58 mm).
This measure relates to the total ability of the substrate to resist both surface
spreading and sub-surface penetration and spreading (within the top coating layer
and layers below) over long times. A hydrophobic surface leads to a smaller stain
diameter than the initial droplet diameter. This method can be used to rank the samples'
performance regarding hydrophobicity.
Initial contact angle measurement
[0105] Short-time contact angles of drops of deionized water (i.e. without the blue dye)
on the coated sheets are measured manually with a Ramé-Hart goniometer, using the
same autopipette, drop volume and procedure (i.e. 5 drops at different places) as
in the staining experiments described above. The time from contact to measurement
of advancing angle is approximately 10 s. This is a standard measure of short-term
hydrophobicity, reflecting the ability of the substrate to reject water drops on first
contact. The use of a manual goniometer is convenient because the drop can roll or
hop on initial contact with a highly hydrophobic or superhydrophobic substrate.
Rolling angle measurement
[0106] The drop rolling tests are performed using a tilt table. The same blue dye solution
as mentioned above is autopipetted in a similar manner as in the stain test on the
coated samples pre-inclined at 5 fixed angles (2.5, 5, 10, 15 and 20° from horizontal).
The lowest angle for which free rolling occurs, i.e. the drop rolls the entire distance
of the sample size (around 10 cm), is the value assigned to the substrate. Failure
to roll freely at 20° is regarded as a no-score, despite the fact that free rolling
may occur at higher angles not tested (e.g. approaching vertical). It is expected
that drop rolling is closely dependent on advancing initial contact angle (see above).
Example 1
[0107] Precipitated calcium carbonate (PCC) (Sturcal F, Specialty Minerals Inc.) (Particle
size D
50 ca 2.5 µm, apparent density 0.32-0.43 g/ml, and BET surface area ca 6 m
2/g) particles were mixed together with water and a sodium oleate solution in a glass
beaker with a magnetic stirrer. The total content of calcium carbonate in water was
30 wt% and the content of sodium oleate was 1 wt% per pigment weight (dry on dry).
This suspension was mixed until it was essentially homogenous. Further, 30 wt% per
pigment weight (dry on dry) of commercially available styrene-butadiene (SB) latex
(DL 940, The Dow Chemical Company) was added to the above-mentioned aqueous suspension
containing sodium oleate and calcium carbonate. This suspension was again mixed with
a magnetic stirrer to obtain an essentially homogenous mixture. The aqueous dispersion
was coated on paper (Performa Natura, 255 g/m
2, Stora Enso). The coating was performed using a bench coater from RK Print-Coat Instruments
Ltd. Several sheets of paper were coated and then dried in an oven at 70 °C for 2
minutes.
[0108] Water contact angle on coated paper was characterized by Ramé Hart goniometer. The
analysis performed for coatings are explained thoroughly above. For the above-mentioned
coating the contact angle was 140° and the normalized stain size was 1.0. The rms
roughness of the coated substrate measured by Zygo white light interferometric profilometer
(NewView 5010, Zygo Corporation) was below 1.2 µm for following length scales: 0-5
µm, 5-10 µm, 10-20 µm, 20-40 µm, 40-80 µm and 80-170 µm.
Example 2
[0109] The formulation of Example 1 was modified by having 50 wt% per pigment weight of
the same SB-latex binder (DL 940, The Dow Chemical Company) instead of 30 wt% per
pigment weight as used in Example 1. The coating and the analysis were performed as
in Example 1. For this coated substrate the contact angle was 120° and the normalized
stain size was 1.4. The rms roughness measured by Zygo whitelight interferometric
profilometer was below 1.2 µm for following length scales: 0-5 µm, 5-10 µm, 10-20
µm, 20-40 µm, 40-80 µm and 80-170 µm.
Example 3
[0110] The formulation of Example 1 was modified by having 17 wt% per pigment of the same
SB-latex binder (DL 940, The Dow Chemical Company) instead of 30 wt% per pigment as
used in Example 1. The coating and the analysis were performed as in Example 1. For
this coated substrate the contact angle was 145° and the normalized stain size was
2.5.
Example 4
[0111] The formulation of Example 1 was modified by having 2 wt% per pigment weight of sodium
oleate instead of 1 wt% per pigment weight as used in Example 1. The coating and the
analysis were performed as in Example 1. For this coated substrate the contact angle
was 142° and the normalized stain size was 0.8. Water droplets (9 µl) showed rolling
at 15° inclination.
Example 5
[0112] The formulation of Example 1 was modified by having 3 wt% per pigment weight of sodium
oleate instead of 1 wt% per pigment weight as used in Example 1. The coating and the
analysis were performed as in Example 1. For this formulation the contact angle was
154° and the normalized stain size was 0.8. Water droplets (9 µl) showed rolling at
10° inclination.
Example 6
[0113] The formulation of Example 1 was modified by having 2 wt% per pigment weight of sodium
oleate instead of 1 wt% per pigment weightas used in Example 1. Further, the formulation
in Example 1 was modified by having 40 wt% per pigment weight of the same SB-latex
binder (DL 940, The Dow Chemical Company) instead of 30 wt% per pigment. The coating
and the analysis were performed as in Example 1. For this coated substrate the contact
angle was 146° and the normalized stain size was 0.9. Water droplets (9 µl) showed
rolling at 20° inclination.
Example 7
[0114] The formulation of Example 1 was modified by changing the pigment to another type
of PCC calcium carbonate, Sturcal H (Specialty Minerals Inc.). (Particle size D
50 4.0 µm, apparent density 0.48-0.61 g/ml, and BET surface area ca 5 m
2/g) Further, the formulation in Example 1 was modified by adding 2 wt% per pigment
of sodium oleate instead of 1 wt% per pigment as used in Example 1. The coating and
the analysis were performed as in Example 1. For this coated object the contact angle
was 153° and the normalized stain size was 0.6. Water droplets (9 µl) showed rolling
at 5° inclination.
Example 8
[0115] The formulation of Example 7 was modified by changing the SB-latex binder to an experimental
grade SB-latex (SB/HPQ73, The Dow Chemical Company). The SB-latex content was again
30 wt% per pigment weight. The coating was performed on commercially available paper
(Cupforma Classic, 230 g/m
2, Stora Enso). Otherwise the coating and analysis was performed as in Example 1. For
this coated substrate the contact angle was 143° and the normalized stain size was
0.6. Water droplets (9 µl) showed rolling at 10° inclination.
Example 9
[0116] The formulation of Example 8 was modified by increasing the total solids content
of the coating from 34 wt% to 51 wt%. Otherwise the coating and analysis were performed
as in Example 8. For this coated substrate the contact angle was 160° and the normalized
stain size was 0.5. Water droplets (9 µl) showed rolling at 2.5° inclination.
Example 10
[0117] The formulation of Example 8 was modified by adding commercially available ammonium
zirconium crosslinker (Allicross AZC-R, Allinova). The crosslinker content was 4 wt%
dry based on dry binder weight. Otherwise the coating and analysis were performed
as in Example 8. For this coated substrate the contact angle was 141° and the normalized
stain size was 0.6. Water droplets (9 µl) showed rolling at 15° inclination.
Example 11
[0118] The formulation of Example 9 was modified by changing the binder to the commercially
available latex Rhodopas Ultradia 7100 (Rhodia). The binder content was 30 wt% per
pigment weight (dry on dry). The coating and analysis were performed as in Example
8. For this coated substrate the contact angle was 155° and the normalized stain size
was 0.6. Water droplets (9 µl) showed rolling at 2.5° inclination.
Example 12
[0119] The formulation of Example 11 was modified by changing the binder to the commercially
available latex Rhodopas Ultradia 7300 (Rhodia). The binder content was again 30 wt%
per pigment weight. The coating and analysis were performed as in Example 8. For this
coated substrate the contact angle was 154° and the normalized stain size was 0.6.
Water droplets (9 µl) showed rolling at 10° inclination.
Example 13
[0120] The formulation of Example 9 was modified by using diphosphonate alkyl surfactant
instead of the sodium oleate. The content of diphosphonate alkyl surfactant was 1
wt% per pigment weight (dry on dry). The coating and analysis were performed as in
Example 8. For this coated substrate the contact angle was 139° and the normalized
stain size was 0.9.
Example 14
[0121] The formulation of Example 13 was modified by changing the diphosphonate alkyl surfactant
content to 2 wt% per pigment weight. The coating and analysis were performed as in
Example 8. For this coated substrate the contact angle was 136° and the normalized
stain size was 0.9.
Example 15
[0122] The formulation of Example 8 was modified by changing the Sturcal H pigment to the
PCC Opacarb A40 (Specialty Minerals Inc.) (Particle size D
50 0.4 µm, density 0.48-0.61 g/ml, and BET surface area 12 m
2/g). Opacarb was removed from the manufacturing process before the addition of dispersant,
because the dispersant is unsuitable in the present formulation. The total solids
content of the formulation was 30 wt%. The coating and analysis were performed as
in Example 8. For this formulation the contact angle was 148° and the normalized stain
size was 0.6. Water droplets (9 µl) showed rolling at 10° inclination.
Example 16
[0123] Aluminium sulfate, Al
2(SO
4)
3.18H
2O was mixed together with water. This solution was mixed with kaolin (Kaolin C, ECC),
(Particle size D
50 <2 µm, density 2.6 g/ml, and BET surface area 10 m
2/g) stirring until it was essential homogenous. Then a 10% solution of sodium carbonate
was added, and the mixture stirred until again homogenous. To this slurry a 5% solution
of sodium oleate was added. The total content of kaolin in the aqueous dispersion
was 29 wt%, the content of sodium oleate was 2.4 wt% per pigment weight (dry on dry),
the content of sodium carbonate was 4.3 wt% on pigment (dry on dry), and the content
of Al
2(SO
4)
3.18H
2O was 9.4 wt% per pigment weight (dry on dry).
The aqueous dispersion was coated on paperboard (Cupforma Classic, 230 g/m
2, Stora Enso). The coating was performed using a bench coater from RK Print-Coat Instruments
Ltd. Several sheets of paper were coated and then dried in an oven at 90 °C for 2
minutes.
[0124] For the above-mentioned coating the contact angle with water was 132°.
Example 17
[0125] To the aqueous dispersion from Example 16, a styrene-butadiene latex binder (HPQ
73, Dow Europe) was added, and the dispersion was stirred until homogeneous. The content
of latex was 30 wt% per pigment weight(dry on dry). The coating and the analysis were
performed as in Example 16. For this coated substrate the contact angle was 113°.
Example 18
[0126] The formulation in Example 17 was modified by increasing the level of the latex HPQ73
to 30 wt% per pigment weight(dry on dry). The coating and the analysis were performed
as in Example 16. For this coated substrate the contact angle was 90°.
Example 19
[0127] Precipitated calcium carbonate (PCC) (Sturcal H, Specialty Minerals Inc.) (Particle
size D
50 4.0 µm, apparent density 0.48-0.61 g/ml, and BET surface area ca 5 m
2/g) particles were mixed together with water and a sodium oleate solution in a glass
beaker with a magnetic stirrer. The total content of calcium carbonate in water was
30 wt% and the content of sodium oleate was 2 wt% per pigment weight (dry on dry).
This suspension was mixed until it was essentially homogenous and then added to the
aqueous dispersion in Example 16 and again mixed until homogeneous. The resulting
ratio of PCC pigment to clay pigment was 70% PCC and 30% clay. To this aqueous dispersion,
a styrene-butadiene latex binder (HPQ 73, Dow Europe) was added, and the dispersion
was stirred until homogeneous. The content of latex was 15 wt% per pigment weight
(dry on dry). The coating and the analysis were performed as in Example 16. For this
coated substrate the contact angle was 123°.
Example 20
[0128] The formulation in Example 19 was modified by changing the ratio of PCC pigment to
clay pigment to 50% PCC and 50% clay (dry on dry). The coating and the analysis were
performed as in Example 16. For this coated substrate the contact angle was 115°.
Example 21
[0129] The formulation of Example 1 was modified by having 2 wt% per pigment of sodium oleate
instead of 1 wt% per pigment weight as used in Example 1. Further, the formulation
in Example 1 was modified by having 30 wt% per pigment weight of another SB-latex
binder (SHY-7, Dow Europe) instead of DL 940. The aqueous dispersion was coated on
paperboard (Cupforma Classic, 230 g/m
2, Stora Enso). The coating was performed using a bench coater from RK Print-Coat Instruments
Ltd. Several sheets of paper were coated and then dried in an oven at 90 °C for 2
minutes.
The coating and the analysis were performed as in Example 1. For this coated substrate
the contact angle was 148° and the normalized stain size was 0.7. Water droplets (9
µl) showed rolling at 2.5° inclination.
Example 22 (comparative, not according to the present invention)
[0130] A comparative formulation was prepared by utilising commercially available dispersant
(Dispex N40, Ciba Specialty Chemicals). As particles, PCC Opacarb A40 (Specialty Minerals
Inc.) (Particle size D
50 0.4 µm, density 2.8 g/ml, and BET surface area 12 m
2/g) was used.
The content of Dispex N40 was 0.05 wt% per pigment weight and no fatty acid or other
surfactant were added. The coating and analysis were performed as in Example 8. For
this formulation the contact angle was 71° and the normalized stain size was 2.1.
Water droplets (9 µl) did not show rolling at any inclination.
1. An aqueous dispersion to be used in the manufacture of a hydrophobic coating, wherein
said aqueous dispersion comprises:
a) inorganic particles
b) at least one fatty acid or a salt thereof,
c) a polymeric binder, and
d) water.
2. The aqueous dispersion according to claim 1, wherein said aqueous dispersion comprises:
a) from about 20 to about 55 wt% of inorganic particles,
b) from about 0.1 to about 2 wt% of at least one fatty acid or a salt thereof
c) from about 5 to about 20 wt% of a polymeric binder, and
d) the rest being water and optional additives.
3. The aqueous dispersion according to any one of claims 1 to 2, wherein said inorganic
particles comprise at least one substance selected from the group consisting of calcium
carbonate and kaolin.
4. The aqueous dispersion according to any one of claims 1 to 3, wherein said inorganic
particles comprise at least one substance selected from the group consisting of anatase,
calcinated clay, kaolin, and talc, the surface of which has been made basic.
5. The aqueous dispersion according to any one of claims 1 to 4, wherein said inorganic
particles comprise at least one substance selected from the group consisting of aluminium
hydroxide, aragonite, barium sulphate, calcite, calcium sulphate, dolomite, magnesium
hydroxide, magnesium carbonate, magnesite, titanium dioxide (rutile), and vaterite.
6. The aqueous dispersion according to any one of claims 1 to 5, wherein said inorganic
particles comprise at least one substance selected from the group consisting of zincite,
corundum, hematite, magnetite, ilmenite, and cassiterite.
7. The aqueous dispersion according to any one of claims 1 to 6, wherein said inorganic
particles comprise at least one substance selected from the group consisting of dispore,
boehmite, goethite, lepidocrocite, rhodocrosite, siderite, baryte, strontianite, apatite,
feldspar and fluorite.
8. The aqueous dispersion according to any one of claims 1 to 7, wherein said inorganic
particles comprise SiO2.
9. The aqueous dispersion according to any one of claims 1 to 8, wherein said inorganic
particles have an apparent density from about 0.30 g/ml to about 4 g/ml.
10. The aqueous dispersion according to any one of claims 1 to 9, wherein said inorganic
particles have a BET specific surface area from about 1 m2/g to about 20 m2/g.
11. The aqueous dispersion according to any one of claims 1 to 10, wherein said inorganic
particles have a D50 of less than 20 µm.
12. The aqueous dispersion according to any one of claims 1 to 11, wherein said fatty
acid or salt thereof has 8 to 22 carbon atoms.
13. The aqueous dispersion according to any one of claims 1 to 12, wherein said fatty
acid is selected from the group consisting of oleic acid, stearic acid and palmitic
acid.
14. The aqueous dispersion according to any one of claims 1 to 13, wherein said fatty
acid salt is a salt of a fatty acid selected from the group consisting of oleic acid,
stearic acid and palmitic acid.
15. The aqueous dispersion according to any one of claims 1 to 14, wherein said polymeric
binder is selected from the group consisting of a carboxylated latex, a styrene-butadiene
latex and a styrene acrylate.
16. The aqueous dispersion according to any one of claims 1 to 15, wherein said aqueous
dispersion further comprises other surfactants.
17. The aqueous dispersion according to claim 16, wherein said surfactant is selected
from the group consisting of phosphoric acid alkyl ester and diphosphonate surfactants
or salts thereof, silicone based surfactants and fluorosurfactants.
18. The aqueous dispersion according to any one of claims 1 to 17 further comprising at
least one additive selected from the group consisting of antioxidants, biocides, coalescence
agents, coloured inorganic particles, crosslinkers, defoaming agents, dyes, coalescence
agents, fungicides, lubricants, optical brighteners, rheology modifiers, or any combination
thereof.
19. A method for preparing an aqueous dispersion according to any one of claims 1 to 18
comprising the step of mixing an aqueous dispersion of a polymeric binder with a mixture
of inorganic particles and at least one fatty acid or a salt thereof.
20. The method according to claim 19, wherein said mixture of inorganic particles and
at least one fatty acid or a salt thereof is prepared by
a) mixing said at least one fatty acid or a salt thereof with water,
b) mixing said inorganic particles with water, and then
c) mixing the mixtures from step a) and step b).
21. The method according to claim 19, wherein said mixture of inorganic particles and
at least one fatty acid or a salt thereof is prepared by
a) mixing at least one fatty acid or a salt thereof with water and then
b) mixing the mixture from step a) with said inorganic particles.
22. The method according to any one of claims 20 to 21, wherein said polymeric binder
is mixed with said inorganic particles at least 15 minutes after the mixing of said
at least one fatty acid or a salt thereof with said inorganic particles.
23. The method according to any one of claims 19 to 22, further comprising a step of making
non-basic inorganic particles basic.
24. The method according to claim 23, wherein said inorganic particles are contacted with
at least one hydrolysable polyvalent metal salt, followed by neutralisation.
25. A method for coating a substrate comprising contacting said substrate with an aqueous
dispersion according to any one of claims 1 to 18.
26. The method according to claim 25, wherein said substrate further is heated after contacting
said substrate with said aqueous dispersion.
27. The method according to any one of claims 25 to 26, wherein said method comprises
at least one method selected from the group consisting of spray coating, dip coating,
roll application, free jet application, blade metering, rod metering, metered film
press coating, air knife coating, curtain coating, flexography printing, roll coating,
and powder coating.
28. A subject coated according to any one of claims 25 to 27, wherein said subject is
highly hydrophobic.
29. The subject according to claim 28, wherein said subject is superhydrophobic.